Process for drying textiles



Dec. 25, 1956 F. B. THIES PROCESS FOR DRYING TEXTILES Original Filed March 18, 1952 INVENTORS.- MM BY W 3mm United States Patent Ofi ice Re. 24,260 Reissued Dec. 25, 1956 PROCESS FOR DRYING TEXTILES Alfred Friedrich Bernhard Thies, Coesfeld, Westphalia,

Germany, assignor to Firma B. Thies, Spezialmaschinenfabrik, Coesfeld, Westphalia, Germany Original No. 2,739,392, dated March 27, 1956, Serial No.

277,100, March 18, 1952. Application for reissue September 11, 1956, Serial No. 609,333

Claims priority, application Germany March 21, 1951 8 Claims. (Cl. 34-15) Matter enclosed in heavy brackets II] appears in the original patent but forms no part of this reissue specification; matter printed in italics indicates the additions made by reissue.

The present invention relates to a process and apparatus for drying textile materials and more particularly to a process and apparatus for drying textile materials more rapidly and at higher temperatures than was hitherto possible.

It is an object of the present invention to provide a process for drying textile materials very rapidly and at relatively high temperatures.

It is a further object of the present invention to provide a process for drying textile materials in a substantially dust-free atmosphere and at temperatures which would normally adversely affect the fibers of the textile material.

It is a still further object of the present invention to provide a process for drying textile materials much more rapidly and more completely than could hitherto be accomplished.

It is another object of the present invention to provide an apparatus for carrying out the above objects of the process of the present invention.

It is still another object of the present invention to provide an apparatus for heating a textile material with heated air in a closed system whereby the moisture absorbed from the textile material is removed from the air, the air is again reheated and the reheated air passed through the textile material so as to effect a complete removal of the moisture from the textile material, the air being maintained in a closed system and thereby being kept substantially dust-free.

Additional objects and advantages of the present invention will be apparentfrom the following disclosure and the claims.

With the above objects in view, the process of the present invention mainly consists in passing heated air under superatmospheric pressure through a textile material containing moisture so that at least a portion of the moisture contained in said textile material is absorbed by said heated air; drying said air under superatmospheric pressure containing absorbed moisture; reheating said thus dried air; and passing said thus dried and reheated air again through said textile material so that the air for drying said textile material is kept in a closed circuit and maintained substantially dust-free, thus drying said textile material in a substantially dust-free atmosphere.

It is a preferred embodiment of the present invention that the textile material is first treated with super-heated steam so that the temperature of the textile material is raised while the specific moisture content of the textile material is lowered. The raising of the temperature of the textile material causes the water contained in the same to be more quickly evaporated in a later step of passing heated air through the textile material. The specific moisture content of the textile material is lowered by the superheated steam since the textile material, before being treated with the steam, is saturated and the raising of the temperature of the textile material causes some of the molsture contained in the same to be evaporated therefrom while the textile material remains saturated at the higher temperature, thereby lowering the specific moisture contents.

It is another preferred embodiment of the present invention to pass the heated air through the textile material under superatmospheric.pressure so that a higher temperature may be employed for evaporating the moisture contained in the textile material without adversely affecting the fibers of the material.

The present invention further provides for passing the heated air through the textile material for the second and perhaps subsequent times in dilferent directions so that a more complete absorption by the heated air of the moisture contained in the textile material can be efiected- The present invention is particularly applicable for drying textile materials such as cross-wound bobbins or yarn in package form which are placed on a special carrier and then placed in a container. Before the present invention, heated air was blown through the material and thus a sufiicient drying effect could be obained only by considerable expenditure of power. Furthermore, the constant sucking-in of fresh air caused the disadvantage of particles of dust and other impurities, as well as moisture contained in the atmosphere of air, being blown into the material to be dried.

On the other hand, the present invention oflers the possibility of using temperatures of so high a degree that they would afiect the fibers when used in a normal drying process; they are, however, admissible owing to the proportionately short time during which, according to the present invention, these high temperatures influence the material and owing to the circulation closed in itself.

The present invention further allows for the drying of the textile material simultaneously with, previous to or after a steam treatment of the same with suitable vaporforming or volatile substances such as plasticizers.

A preferred process of the present invention comprises passing super-heated steam through a textile material saturated with moisture so as to raise the temperature of said textile material while lowering the specific moisture content of the same; removing the excess steam; passing heated air under super-atmospheric pressure through said textile material containing moisture so that at least a portion of the moisture contained in said textile material is absorbed by said heated air and the temperature of the textile material is raised.

The process of the present invention is most advantageously carried out in an apparatus comprising a cham ber; blower means operatively connected to said chamher for blowing air into the same; heater means operatively connected to said blower means for heating the air before it enters said chamber so that heated air is blown into said chamber and through the textile material therein, thereby absorbing moisture from said textile material; first conduit means connected to said chamber for removing said air containing absorbed moisture from the same; extracting means operatively connected to said conduit means for extracting the moisture from said air containing absorbed moisture 'so as to dry said air; and second conduit means operatively connected to said extracting means and to said blower means for passing said dried air from said extracting means to said blower means whereby the air for drying the textile material is carried through a closed circuit throughout the operation.

It is a preferred embodiment of the present invention that the heated air is passed through the textile material to be dried in difierent directions so as to effectuate a more complete drying of'the textile material. Accordingly, the apparatus of the present invention provides a considerable improvement by the use of a suitable reversing means for reversing the direction of the heated air through the chamber. This reversing mechanism may consist of valve means fitted between the inlet and outlet pipes of the chamber, which when turned in one direction causes the heated air to pass into theinlet pipe and the air containing absorbed moisture to pass out of the outlet pipe, and when turned in' anotherdirection causes the outlet pipe to become the inlet pipe and the inlet pipe to become the outlet pipe so that the air is passed through the chamber in a different direction, thereby allowing for a more uniform. drying of the textile material in the .chamber.

The present invention vgreatly. reduces the time of drying, especially when workingunder superatrnospheric pressure, thereby resulting in agreat economy in power. Moreover, contamination of the textile material, which normally occurs with..the.,use of impure, fresh air, is prevented. 'The use of superatmospheric pressure renders it possible to introduce large quantities of heat into the textile. material, which may be contained in wound packages, while the output of the blower remains nearly the same, thus effecting a shortening of the drying time by a more rapid absorption of heat and consequently, by a. quicker evaporation ofthe water. A is well known, the ability ofthe air to absorb heat is considerably increasedinxproportion to the rising pressure, whereby of course thecweight. of the gas respectively of the gas mixture contained in the apparatus is augmented.

The air leaving the chamber .isdried. by means of a water extractor working-With. direct or indirect cooling, which .serves to separate .the water contained in the current of saturated air. Insteadof using a cooling device, water can be directly injected into the Water extractor in order to obtain, by a sudden cooling, a separation of the water from-the air. Also, a separation of the humidity is obtained byv the diminution of the speed of the air entering the water-extractor. Thus, a lowering of the temperature of. the air: sucked intothe blower is efiected so that a proportionally simple pressure-proof blower can be used.

The novel features-which are consideredas characteristic for the invention are set.forth inv particular: in the appended claims. The invention itself, however, :both as to its constructionand its method of. operation, 'together with additional objects:and-advantages thereof,

will "be best understood front-thejollowing-description of specific embodiments :when .=read in connection with the accompanying drawings, in' which' 'the figure is a schematic drawing of an apparatus according to the present invention.

Referring now to the drawinga drying container 11 holding the material tobe.dried. 20. on the carrier 13, i equipped withzan. inside perforated "double casing 21 and two inlets or outlets..2 .and 3. .Both these inlets or outlets lead to a valvemeansi 24 which. is connected through a heating battery'Stoithe blower 7 communicating with the outside .air by means of a valve 1a. This valve means 24 and with it .the container 11 is further- -more connected by another pipe with. the water extractor and through this extractor'also 'tothe' blower 7.

As may be seen, the valve means 24 in one position causes the air blown by. blower 7': through heater 8 to enter the container 11-attherbottom thereof through inlet 2, whereas the air containing absorbed moisture leaves the container ll'throughthe outlet 3 and thence to the water extractor 10. When turned at a 90 angle,

the valve means 24 causes theheated. air passingfrom the blower 7 through the heater 8, to'enter'the container 11 through pipe 3 which-now-becomes an inlet:pipe and to leave the chamber-11- through ,2-rlwhich now-becomes an outlet pipe :and to. .pass: through-1 the-valve--24 .to: the water extractor 10.

" 7 is provided with another valve 17 and a second connection to the outside air through the valve 1b. The water extractor 10 is provided with a cooling device 19 equipped with an inlet 12 and an outlet 23 for the cooling water as well as the outlet 5 to the measuring receptacle. It is further connected by the valve 4 with a compressed gas container 26 and by the valve 22 with an evacuating device 18. The outlet 5 'enters into a measuring receptacle 14 provided with awater level indicator 15.

The water level indicator 15 enables the. operatorato observe the exact progress of thexdrying by ascertaining at what time the receptacle 14 has received the quantity of water known to be contained in the textile material by the previous weighing of the same) Valves 1c, 1d, 1e, and 1f are operated during the process.

The operation of theapparatus is as.follows:

For the steaming .of the material, valves 1c: and 1d are. closed and the vmaterial is. placed. .on thexcarrier 13 in the container 11. Superheatedsteamis. directed through the steam valve 1e under pressure. Valve If is open so as to allow the excess moisture, after the steam has passed through the material 20, .to escape.

Valves 1e and 1f are then closed. Valves 1c and 1d are then openedwhile valves 1a and 1e remain closed. Valve 5 is also closed and compressed gas is sentinto the apparatus'through valve 4 under superatmospheric pressure.

The heating battery 8 is heated and the cool water valve 12 in the water extractorv 10 is open, as is cool water outlet valve 23. Valve 17 is opened so as to start the circulation and the blower 7 is started. The blower 7 causes the air to pass through the heater 8 so that hot air is passed through the valve 24, into the chamber 11 andthrough the material 20. In the positionindicated in the drawing the four-way valve 24 causes the heated air from the heater 8 to pass into the container 11 through inlet 2. As previously described, the four-way valve may be turned so as to cause the heated air to pass into the container 11 through valve 3.

In the position shown in the drawing, the heated air enters the chamber through valve 2, passes through the material 20, leaves the chamber through the valve 3 and is thereby directed-to the water extractor 10. Through the sudden expansion of the air containing absorbed Water in thewater extractor 10,'-combined with the cooling device 19, the moisture content of the air: is lowered. The waterrernoved from the air-is passed through valve 5 into the measuring-receptacle 14 with the water level indicator 15.

The air, with the water removed therefrom, passes through valve17 and by,means of the blower 7 is again forced into the heater 8 and then into the container 11.

The apparatus and process of the present invention allows for a saving of about 50% .in the time required to dry textile material by ordinary processes.

It will be understood that each of :the elements described above, or two or more together, may also find a useful application in other types of drying apparatus and processes differing from the types described above.

While the invention has been illustrated and described as embodied in an apparatus'andprocess for drying textilematerials, it is not intended'to be limited'to the details shown, since various modifications and structural changes may be made without departing in any way from the spirit of the present invention.

Without further analysis, the foregoing will so fully reveal the gist of the present invention that others can by applying current knowledge readily adapt it for variousapplications without omitting features that, from the standpoint of prior art, fairly constituteessentialchar- :acteristics of the-generic or. specific aspects. ofthis-in- 5 intended to be comprehended within the meaning and range of equivalence of the following claims.

What is claimed as new and desired to be secured by Letters Patent is:

1. A process for drying textile materials, comprising, in combination, the steps of passing under superatmospheric pressure heated air [under superatmospheric pressure] through a textile material containing moisture so that at least a portion of the moisture contained in said textile material is absorbed by said heated air under superatmospheric pressure and said heated air leaves said textile material under superatmospheric pressure and containing moisture absorbed from said textile material; drying said air containing absorbed moisture; reheating said thus dried air; and passing said thus dried and reheated air again through said textile material so that the air for drying said textile material is kept in a closed circuit and maintained substantially dust-free, thus drying said textile material in a substantially dust-free atmosphere.

2. A process for drying textile materials, comprising, in combination, the steps of passing super-heated steam through a textile material saturated with moisture so as to raise the temperature of said textile material while lowering the specific moisture content of the same; passing under superatmospherie pressure heated air [under superatrnospheric pressure] through said textile material containing moisture so that at least a portion of the moisture contained in said textile material is absorbed by said heated air under superatmospheric pressure and said heated air leaves said textile material under superatmospheric pressure and containing moisture absorbed from said textile material; drying said air containing absorbed moisture; reheating said thus dried air; and passing said thus dried and reheated air again through said textile material so that the air for drying said textile material is kept in a closed circuit and maintained substantially dust-free, thus drying said textile material in a substantially dust-free atmosphere.

3. A process for drying textile materials, comprising, in combination, the steps of passing under superatmospheric pressure heated air [under superatmospheric pressure] through a textile material containing moisture so that at least a portion of the moisture contained in said textile material is absorbed by said heated air under superatmospheric pressure and said heated air leaves said textile material under superatmospheric pressure and containing moisture absorbed from said textile material; drying said air containing absorbed moisture; reheating said thus dried air; and passing said thus dried and re heated air again under superatrnospheric pressure through said textile material so that the air for drying said textile material is kept in a closed circuit and maintained substantially dust-free, thus drying said textile material in a substantially dust-free atmosphere.

4. A process for drying textile materials, comprising, in combination, the steps of passing super-heated steam through a textile material saturated with moisture so as to raise the temperature of said textile material while lowering the specific moisture content of the same; passing under superatm-ospheric pressure heated air [under super atmospheric pressure] through said textile material containing moisture so that at least a portion of the moisture contained in said textile material is absorbed by said heated air under superatmospheric pressure and said heated air leaves said textile material under superatmospheric pressure and containing moisture absorbed from said textile material; drying said air containing absorbed moisture; reheating said thus dried air; and passing said thus dried and reheated air under superatmospheric pressure again through said textile material so that the air for drying said textile material is kept in a closed circuit and maintained substantially dust-free, thus drying said textile material in a substantially dustfree atmosphere,

'5, A process for drying textile material s, comprising, in combination, the steps of passing under superatmospheric pressure heated air [under superatmospheric pressure] through a textile material containing moisture so that at least a portion of the moisture contained in said textile material is absorbed by said heated air under super atmospheric pressure and said heated air leaves said textile material under superatmospheric pressure and containing moisture absorbed from said textile material; drying said air containing absorbed moisture; reheating said thus dried air; and passing said thus dried and reheated air again through said textile material in a direction dilferent from the direction through which said heated air was first passed through said textile material so that the air for drying said textile material is kept in a closed circuit and maintained substantially dust-free, thus drying said textile material in a substantially dust-free atmosphere.

6. A process for drying textile materials, comprising, in combination, the steps of passing under superatmospheric pressure heated air [under superatrnospheric pressure] through a textile material containing moisture so that at least a portion of the heat contained in said heated air is transferred to said textile material so that at least a portion of the moisture contained therein is evaporated and absorbed by said heated air under superatmospheric pressure and said heated air leaves said textile material under superatmospheric pressure and containing moisture absorbed from said textile material; cooling said air containing evaporated and absorbed moisture thereby condensing the latter and separating it from said air so as to dry the same; reheating said thus dried air; and passing said thus dried and reheated air again through said textile material so that the air for drying said textile materials is kept in a closed circuit and maintained substantially dust-free, thus drying said textile material in a substantially dust-free atmosphere.

7. A process for drying textile materials, comprising, in combination, the steps of passing under superatmospheric pressure heated air [under superatmospheric pressure] through a textile material containing moisture so that at least a portion of the heat contained in said heated air is transferred to said textile material so that at least a portion of the moisture contained therein is evaporated and absorbed by said heated air under superatmospheric pressure and said heated air leaves said textile material under superatmospheric pressure and containing moisture absorbed from said textile material; cooling said air containing evaporated and absorbed moisture thereby condensing the latter and separating it from said air so as to dry the same; reheating said thus dried air; and passing said thus dried and reheated air again under superatmospheric pressure through said textile material so that the air for drying said textile material is kept in a closed circuit and maintained substantially dust-free, thus drying said textile material in a substantially dustfree atmosphere.

8. A process for drying textile materials, comprising, in combination, the steps of passing under superatmospheric pressure heated air [under superatmospheric pressure] through a textile material containing moisture so that at least a portion of the heat contained in said heated air is transferred to said textile material so that at least a portion of the moisture contained therein is evaporated and absorbed by said heated air under superatmospheric pressure and said heated air leaves said textile material under superatmospheric pressure and containing moisture absorbed from said textile material; cooling said air containing evaporated and absorbed moisture thereby condensing the latter and separating it from said air so as to dry the same; reheating said thus dried air; and passing said thus dried and reheated air again through said textile material in a direction different from the direction through which said heated air was first passed through said textile material so that the air for drying said textile -material is kepta closed 1611161111. and. .maintained sub- 4 stantiallydmt-free, thus dryingsaid texti1e:material in a substantially dust-free atmosphere.

References Cited in the file ofthis patent or the original patent 1 UNITED 'STATES PATENTS 822,239 Bedortha-et a1 -iJune5y1906 1,166,819 Derby et a1. Janz4, 1916 1,324,072 Shorrnan Dec. 9, 1919 1,415,623 Atkinson May 9, 1922 1,524,567 Plews 1:111:27,- 1925 1,540,926 Brandwo'odet a1 June 9, 1925 .cKrantz May. 27, .1927 Brown Dec. 11, .1928 Merriam et a1.v =May 11, 1937 Goodings Feb, 22, 1938 Pugh Oct. 19,1948 Morrison Sept. 5, 1950 Honegger May 6, 1952 FOREIGN PATENTS Germany July 16, 1929 OTHER REFERENCES Drying by Means of Air and Steam, by E. Hausbrand.

Published 1924. Pages 45 to 47 relied on. 

